WO2009112128A1 - Echangeur thermique à plaque, plaque d’échangeur thermique et leur procédé de fabrication - Google Patents

Echangeur thermique à plaque, plaque d’échangeur thermique et leur procédé de fabrication Download PDF

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Publication number
WO2009112128A1
WO2009112128A1 PCT/EP2009/000568 EP2009000568W WO2009112128A1 WO 2009112128 A1 WO2009112128 A1 WO 2009112128A1 EP 2009000568 W EP2009000568 W EP 2009000568W WO 2009112128 A1 WO2009112128 A1 WO 2009112128A1
Authority
WO
WIPO (PCT)
Prior art keywords
heat exchanger
plate
exchanger plate
heat
connection areas
Prior art date
Application number
PCT/EP2009/000568
Other languages
German (de)
English (en)
Inventor
Friedrich Schenker
Volker Wagner
Original Assignee
Api Schmidt-Bretten Gmbh & Co. Kg
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Api Schmidt-Bretten Gmbh & Co. Kg filed Critical Api Schmidt-Bretten Gmbh & Co. Kg
Priority to EP09720512A priority Critical patent/EP2250457B1/fr
Priority to CN2009801085216A priority patent/CN101970968B/zh
Priority to DK09720512.4T priority patent/DK2250457T3/da
Priority to US12/921,800 priority patent/US8770268B2/en
Publication of WO2009112128A1 publication Critical patent/WO2009112128A1/fr

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/08—Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
    • F28F3/083—Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning capable of being taken apart
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0043—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
    • F28D9/005—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • F28F19/02—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings
    • F28F19/06—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings of metal
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/08—Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081—Heat exchange elements made from metals or metal alloys
    • F28F21/082—Heat exchange elements made from metals or metal alloys from steel or ferrous alloys
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/4935—Heat exchanger or boiler making

Definitions

  • the present invention relates to a heat exchanger plate according to the preamble of patent claim 1 for a plate heat exchanger with in the plate plane juxtaposed flow openings for fluid media, which is made of a first material, in particular steel or stainless steel.
  • the present invention relates to a plate heat exchanger according to the preamble of claim 10 for fluid media with at least one inlet and at least one outlet for a first, especially less aggressive medium, with at least one inlet and at least one outlet for a second, more aggressive medium and with a A number of heat exchanger plates operatively connected in fluid communication with the inlets and outlets in the plate heat exchanger.
  • the present invention relates to a method for producing a heat exchanger plate according to the invention.
  • Plate heat exchangers of the aforementioned type are known, for example, from EP 0 252 275 A2 and shown by way of example in the appended FIG.
  • Figure 1 shows an exploded view of a known heat exchanger in which between end plates 1, 2 a package of substantially rectangular, mutually identical and alternately clamped against each other by 180 ° rotated heat exchanger plates 3 is clamped.
  • flow openings 4-7 are formed, the result in clamped plate packs, as shown at reference numeral 8, channels 9-12, over the two fluid media for mutual heat exchange alternately formed spaces between the plates 3 be supplied.
  • the flow openings 4 - 7 may alternatively or additionally also be arranged in other plate areas, in particular the longitudinal sides of the plates.
  • the existing between the plates 3 spaces for the fluid media are sealed to the outside and alternately to the channels of a medium or the other medium in each case by seals 13, so that in each case one plate gap of the one medium, the following plate gap of the other Medium is flowed through.
  • the four sockets 14 attached to the end plate 2 on the outside serve as connection for the supply and discharge of the two media.
  • the heat exchanger plates 3 are guided between the end plates 1 and 2 by engaging in recesses of the plates 3 rods, of which in Figure 1, only the lower rod 15 is shown explicitly.
  • the terminals can also be arranged on the other end plate 1.
  • the invention has for its object to further develop heat exchanger plates of the type mentioned in such a way that they are also suitable for very aggressive media, without that the aforementioned costs disadvantages. At the same time, a method for producing corresponding heat exchanger plates should be specified.
  • the invention solves the problem with regard to the heat exchanger plate having the features of patent claim 1, and with regard to the manufacturing method having the features of patent claim 11.
  • a heat exchanger plate for a plate heat exchanger with in the plate plane juxtaposed throughflow openings for fluid media which is made of a first material, in particular steel or stainless steel, characterized in that the heat exchanger plate substantially only in such subregions of its surface on its front and / or back, in which the heat exchanger plate comes into contact with a particular, in particular relatively aggressive, of the fluid media, consists of another material or is occupied therewith.
  • the present invention provides a method for producing a heat exchanger plate for a plate heat exchanger with in the plate plane juxtaposed flow openings for fluid media, wherein a first raw sheet, the heat exchanger plate in a first material, such as steel, in particular stainless steel is formed, and then the blank sheet his coming into contact with the media surfaces, at least in some areas with a second, in particular higher quality material is occupied. Subsequently, the forming then takes place to the finished heat exchanger plate.
  • a first material such as steel, in particular stainless steel
  • the second material of higher quality, d. H. is more resistant to corrosion than the first material, wherein the second material is preferably high-alloy stainless steels, titanium, tantalum or the like.
  • a possible combination of materials for the heat exchanger plate according to the invention thus provides that this is basically made of the usual material, such as steel or stainless steel, and placed on it, at least in some areas with a higher quality material occupied.
  • the second material in the said subregions is applied to the first material by alitizing, anodizing, sherardizing, inchromizing, phosphating, enameling, plating, spraying, hot dipping, galvanically, but in particular by soldering, brazing or welding.
  • the heat exchanger plate in a large-area, the heat-transferring serving area and the flow-connected terminal portions of the one medium is applied, whereas it is acted upon in two or more adjacent terminal portions, which serve the passage of the other medium from this other medium.
  • the conditions are then reversed.
  • the acted upon by different media areas are each separated by seals.
  • the plate is either occupied only in the two relatively small connection areas for the aggressive medium with the more corrosion-resistant material or additionally in the heat exchanging area connected thereto.
  • the main saving results on that side of the plate, which is acted upon by the less aggressive medium, because there only the relatively small connection areas for the passage of the aggressive medium with the more corrosion-resistant material to be occupied. It is within the scope of the invention, the plate on the side where it is applied over a large area of the aggressive medium to produce continuously from the higher quality material. But it is particularly advantageous to save the two connection areas for the passage of the less aggressive medium and to occupy with the less expensive, less corrosion-resistant material.
  • the wall thickness of the higher-grade material occupancy as well as the less high-quality material occupancy should preferably be the same for cost reasons, so that no material offset must be bridged with additional effort to the circumferentially circumferential edge seals the plates.
  • a heat exchanger plate according to the invention is advantageously only in such sub-areas on its front and / or back with the second, especially higher-grade material is occupied, where this is actually required due to a given media contact, so as to achieve the desired cost advantages ,
  • Figure 1 is an exploded perspective view of a known plate heat exchanger
  • Figure 2 is a schematic front view of a heat exchanger plate according to the invention for a large-area contact with an aggressive medium
  • Figure 3 is a schematic front view of a heat exchanger plate according to the invention for a large-area contact with a less aggressive medium
  • Figure 4 is a schematic representation of the top of a blank sheet for
  • Figure 4a is a sectional view taken along the line A-A in Figure 4;
  • Figure 4b is a sectional view taken along the line B-B in Figure 4;
  • FIG. 5 shows the blank top side for the heat exchanger plate according to the invention in FIG. 3;
  • Figure 5a is a sectional view taken along the line C-C in Figure 6a;
  • Figure 5b is a sectional view taken along the line D-D in Figure 6a.
  • a plate heat exchanger of the type shown in Figure 1 and explained above is known in the art as such.
  • the present invention is particularly concerned with the problem that arises when one of the media supplied to the plate heat exchanger is a relatively aggressive medium capable of attacking the material of the heat exchanger plates 3, in particular by corrosion.
  • the present invention provides to produce the heat exchanger plates 3 locally of a more corrosion resistant material.
  • the different types of materials are represented by different hatching.
  • a uniform hatching consisting of solid lines denotes a (relatively) low-grade material
  • a hatching of solid and dashed lines denotes a relatively high quality, more corrosion resistant material.
  • the high-grade material is advantageously tantalum (Ta) and the low-grade material is stainless steel, but the present invention would not be limited to such material combinations.
  • FIG 2 shows schematically a heat exchanger plate 3a with its intended for an aggressive or corrosive medium front; that is, this side faces a plate gap which is fed with the aggressive medium.
  • it could be according to the invention occupied on its front side over its entire surface with the higher quality material.
  • the plate area effectively acted upon by the aggressive medium is limited by the conventional seal 13a defining the heat exchanging area, the areas of the plate face not coming into contact with the aggressive medium may be made of the conventional base material or may be occupied therewith , These areas could begin immediately at the seal 13a, such as at the lowest point of the seal groove or externally adjacent.
  • connection areas around the openings 5 and 7 around ie to those openings, which are flowed through by the less aggressive medium and surrounded by the usual seals 5a and 7a, to produce from the lower-cost base material or thus occupy.
  • These areas are marked by reference numerals 16a and 17a. They preferably extend to the middle of the narrow plate side. From there they run in the direction of the seal 13a and then bend into the intermediate region between the seals 5a, 7a and 13a until they reach the plate broadside.
  • the plate 3b following the heat exchanger plate 3a is shown with its front side in FIG. It has the same sealing configuration as the back of the plate 3a, that is, the intermediate space formed between the two plates is acted upon by the less aggressive medium supplied through the openings 5 and 7.
  • the area enclosed by the seal 13 b heat exchanging surface 18 b with the openings 5 and 7 surrounding connection areas 16b and 17b are made of the less expensive, less resistant material
  • the connection areas 19b and 20b with the seals 4b and 6b surrounded openings 4 and 6 are made of the more resistant material or must be occupied, because in these openings the more aggressive medium flows.
  • connection areas 16a, b; 17a, b; 19a, b; 20a, b the same size and contour, so that the plate gets a symmetrical structure so far.
  • the plates 3a and 3b may be profiled in a known manner by ribs, nubs or the like in order to improve the heat transfer.
  • unfinished sheet means that the blank sheets already plated or occupied have not yet been further processed (for example, reshaped or provided with flow openings) to make the ready-to-use heat exchanger plates.
  • the blank sheet 3a 'according to FIG. 4 is provided for producing the heat exchanger plate according to FIG. 2 and accordingly has the low-grade material on its illustrated front in right, upper and lower connection regions 16a and 17a, whereas in the main heat-exchanging region 18a and connected to it in fluid communication End regions 19a, 20a left top and bottom consists of the high quality material.
  • Figures 4a and 4b show the cross sections A-A and B-B. It can be seen in the upper half of Figure 4a the already designated material transition between highly corrosion resistant and less corrosion resistant material, whereas the lower portion of Figure 4a shows the conditions on the back of the plate, where passes through the less high-quality material.
  • FIG. 4b The conditions in FIG. 4b are different. Here runs on the front of the plate of more corrosion-resistant material, whereas at the rear of the higher quality material is required only in the connection area 19b, but not in the adjacent large-area heat exchanging surface 18b.
  • FIG. 5 shows a blank sheet 3b 'for heat exchanger plates, which are acted upon by their front side primarily by the less aggressive medium.
  • FIGS. 5a and 5b show sectional views along the line C-C and the line D-D in FIG. 5, respectively.
  • connection areas 16b, 17b right above and below from the less corrosion-resistant material
  • connection areas 19a, 20b for the more corrosive medium left above and bottom made of more corrosion resistant material.
  • connection area 16b, 18b is made continuously of the less corrosion-resistant material whereas the plate rear side only has this material in the connection area 16a for the less aggressive medium.
  • Figure 2 and the corresponding figure 4 and 4a in the front position to the connection areas 16a and 17a are dispensed with, so that there only the backsheet 18b is present.
  • the occurring halving in the panel wall thickness can be bridged by a correspondingly stronger seal 5a and 7a.
  • This single-layer design is particularly advantageous in those connection regions which consist of the higher-grade, more corrosion-resistant material.
  • the connection regions 19b and 20b could be dispensed with and the resulting halving of the plate thickness compensated by correspondingly thicker seals 4b and 6b.
  • heat exchanger plates are provided for a plate heat exchanger in this way, which are able to withstand the action of a relatively aggressive medium, without the entire plate would have to be formed in a high quality and correspondingly more expensive material.

Abstract

Une plaque d’échangeur thermique (3a) pour un échangeur thermique à plaque pourvu d’ouvertures d’écoulement (4 à 7), disposées les unes à côté des autres dans le plan de la plaque, pour des milieux fluides, qui est formée dans un premier matériau, en particulier de l’acier ou de l’acier inoxydable, se caractérise en ce qu’elle est formée ou recouverte sur ses surfaces (18a, 19a, 20a), venant en contact avec un des milieux fluides, avec un autre matériau qui est en particulier plus résistant à la corrosion que le premier matériau.
PCT/EP2009/000568 2008-03-10 2009-01-29 Echangeur thermique à plaque, plaque d’échangeur thermique et leur procédé de fabrication WO2009112128A1 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
EP09720512A EP2250457B1 (fr) 2008-03-10 2009-01-29 Echangeur thermique à plaque, plaque d échangeur thermique et leur procédé de fabrication
CN2009801085216A CN101970968B (zh) 2008-03-10 2009-01-29 板式换热器、换热板及换热板的制造方法
DK09720512.4T DK2250457T3 (da) 2008-03-10 2009-01-29 Pladevarmeveksler, varmevekslerplade og fremgangsmåde til fremstilling deraf
US12/921,800 US8770268B2 (en) 2008-03-10 2009-01-29 Plate-type exchanger, heat exchanger plate and method for producing same

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102008013358A DE102008013358A1 (de) 2008-03-10 2008-03-10 Plattenwärmetauscher, Wärmetauscherplatte und Verfahren zu deren Herstellung
DE102008013358.2 2008-03-10

Publications (1)

Publication Number Publication Date
WO2009112128A1 true WO2009112128A1 (fr) 2009-09-17

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ID=40568247

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2009/000568 WO2009112128A1 (fr) 2008-03-10 2009-01-29 Echangeur thermique à plaque, plaque d’échangeur thermique et leur procédé de fabrication

Country Status (7)

Country Link
US (1) US8770268B2 (fr)
EP (1) EP2250457B1 (fr)
CN (1) CN101970968B (fr)
DE (1) DE102008013358A1 (fr)
DK (1) DK2250457T3 (fr)
PT (1) PT2250457E (fr)
WO (1) WO2009112128A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102605404A (zh) * 2012-04-19 2012-07-25 广东永利坚铝业有限公司 一种铝型材阳极氧化槽液热交换方法及热交换装置

Families Citing this family (7)

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Publication number Priority date Publication date Assignee Title
SE535209C2 (sv) * 2010-06-15 2012-05-22 Alfa Laval Corp Ab Korrosionsbeständig plattvärmeväxlare med tantalhaltig beläggning
JP6061271B2 (ja) * 2013-01-28 2017-01-18 三菱重工業株式会社 プレート式熱交換器の開放要領
TR201811573T4 (tr) * 2013-12-13 2018-09-21 Alfa Laval Corp Ab Plakalı ısı değiştiriciyi üretmeye yönelik yöntem ve plakalı ısı değiştirici.
JP6196908B2 (ja) * 2014-01-24 2017-09-13 株式会社日阪製作所 プレート式熱交換器
DK2957851T3 (en) * 2014-06-18 2017-08-07 Alfa Laval Corp Ab HEAT TRANSFER PLATE AND PLATE HEAT EXCHANGERS THAT INCLUDE SUCH A HEAT TRANSFER PLATE
CN108188524A (zh) * 2018-01-16 2018-06-22 向海星 一种钢不锈钢复合板材制板型散热器
DE102021206945A1 (de) 2021-07-01 2023-01-05 Mahle International Gmbh Wärmeübertragungseinheit

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GB2085144A (en) * 1980-10-14 1982-04-21 Schiffbau Veb K Plate heat exchangers
FR2544060A1 (fr) * 1983-04-06 1984-10-12 Kammerer F Gmbh Plaque d'echange thermique
EP0252275A2 (fr) 1986-07-03 1988-01-13 W. Schmidt GmbH & Co. KG Echangeur de chaleur à plaques
EP0671240A1 (fr) * 1994-03-07 1995-09-13 Texas Instruments Incorporated Structure d'échangeur de chaleur, matériau la constituant et une méthode de réalisation de ce matériau

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Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2085144A (en) * 1980-10-14 1982-04-21 Schiffbau Veb K Plate heat exchangers
FR2544060A1 (fr) * 1983-04-06 1984-10-12 Kammerer F Gmbh Plaque d'echange thermique
EP0252275A2 (fr) 1986-07-03 1988-01-13 W. Schmidt GmbH & Co. KG Echangeur de chaleur à plaques
EP0671240A1 (fr) * 1994-03-07 1995-09-13 Texas Instruments Incorporated Structure d'échangeur de chaleur, matériau la constituant et une méthode de réalisation de ce matériau

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102605404A (zh) * 2012-04-19 2012-07-25 广东永利坚铝业有限公司 一种铝型材阳极氧化槽液热交换方法及热交换装置

Also Published As

Publication number Publication date
DE102008013358A1 (de) 2009-09-17
PT2250457E (pt) 2013-03-18
CN101970968B (zh) 2013-11-13
EP2250457A1 (fr) 2010-11-17
CN101970968A (zh) 2011-02-09
DK2250457T3 (da) 2013-04-02
US8770268B2 (en) 2014-07-08
EP2250457B1 (fr) 2012-12-26
US20110011571A1 (en) 2011-01-20

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